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Method for treating high-ammonia-nitrogen wastewater by feeding polyurethane filler

A technology of polyurethane filler and high ammonia nitrogen, which is applied in aerobic process treatment, anaerobic digestion treatment, chemical instruments and methods, etc., can solve problems such as secondary pollution, affecting the operation of biochemical systems, and affecting coal chemical enterprises, etc., to increase the load ability and impact resistance, increase sludge concentration and stability, and achieve harmless and resourceful effects

Inactive Publication Date: 2018-09-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The problem of high ammonia nitrogen wastewater treatment has seriously affected the development of coal chemical enterprises. Conventional biochemical methods are used to treat high ammonia nitrogen wastewater, often requiring multi-stage processes in series and difficult to achieve discharge standards after treatment. There are problems such as complex processes and high treatment costs.
[0003] A coal chemical company in Ningxia produces 1t / h of high-ammonia-nitrogen wastewater, with an ammonia-nitrogen concentration of 3000mg / L. The discharge of ammonia-nitrogen wastewater into the water will cause serious environmental pollution, causing water eutrophication, black and odorous water, and other problems, and has a toxic effect on people and organisms.
Faced with the country's restrictions on the discharge of coal gasification wastewater and the requirement of 100% reuse, it is difficult to achieve satisfactory results in the treatment of the wastewater by traditional biochemical treatment processes, which limits the further development of coal chemical enterprises
[0004] The conventional treatment method for high ammonia nitrogen wastewater is to blow off nitrogen and then proceed to biochemical treatment. However, because the biochemical system has high requirements for ammonia nitrogen in the influent, the concentration of ammonia nitrogen after blowing off nitrogen often cannot meet the water requirements of the biochemical system. At this time, the ammonia nitrogen wastewater enters the biochemical system. After the system, it will impact the biochemical sludge and affect the normal operation of the biochemical system
[0005] The patent "Ammonia Nitrogen Recovery Equipment, Multi-stage Ammonia Nitrogen Wastewater Treatment System" (application number: 201510171724.7) discloses a kind of ammonia nitrogen recovery equipment, which adjusts the pH of ammonia nitrogen wastewater to an appropriate value through the pH value control unit, and then goes to the thin film distillation unit and electrodialysis unit After treatment, the removal and recovery of ammonia nitrogen has been realized, but there are problems such as complicated process and long treatment time
[0006] "Experimental Research on the Treatment of High Ammonia Nitrogen Wastewater by Electrochemical Oxidation" (Lu Jian, Safety and Environmental Engineering, 2010, 17(2):51-53) In view of the secondary pollution and high ammonia nitrogen value of the effluent in the traditional high ammonia nitrogen wastewater treatment process, etc. The problem is that the electrochemical oxidation method is used to test and study the high ammonia nitrogen water distribution. The results show that the concentration of ammonia nitrogen can be reduced from 2000mg / L to 247.51mg / L after electrolysis for 90 minutes. application prospects, but there are problems such as complex process and high cost

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Take high ammonia nitrogen wastewater, the ammonia nitrogen content is 3000mg / L, and the COD concentration is 600mg / L.

[0043] Add sodium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 10.5, enter the airtight reaction column for aeration, the aeration rate is 100L / L / h (air / water / hour), the aeration time is 90min, and the gas outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 300mg / L after blowing off the nitrogen.

[0044] Add hydrochloric acid to the wastewater after blowing off nitrogen to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2000, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 20 hours.

[0045] The effluent of the aerobic tank was added with 500mg / L glucose as an additional carbon source, and entered into the anoxic tank for reaction, and the anoxic tank was filled ...

Embodiment 2

[0048] Take high ammonia nitrogen wastewater, the ammonia nitrogen content is 3200mg / L, and the COD concentration is 550mg / L.

[0049]Add potassium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 11, enter the airtight reaction column for aeration, the aeration rate is 120L / L / h (air / water / hour), the aeration time is 70min, and the air outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 320 mg / L after blowing off the nitrogen.

[0050] Add hydrochloric acid to the wastewater after nitrogen removal to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2400, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 15 hours.

[0051] Add 600mg / L of sodium acetate as an external carbon source to the effluent of the aerobic tank, and enter the anoxic tank for reaction. The anoxic tank is filled with 50% polyur...

Embodiment 3

[0054] Take high ammonia nitrogen wastewater with an ammonia nitrogen content of 3500mg / L and a COD concentration of 700mg / L.

[0055] Add sodium hydroxide to the high ammonia nitrogen wastewater, adjust the pH to 10.8, enter the airtight reaction column for aeration, the aeration rate is 110L / L / h (air / water / hour), the aeration time is 60min, and the air outlet uses acid The separated ammonia gas is recovered and reused, and the concentration of ammonia nitrogen in the waste water is 340mg / L after the nitrogen is blown off.

[0056] Add hydrochloric acid to the wastewater after blowing off nitrogen to adjust the pH to neutral, add sodium bicarbonate to adjust the alkalinity to 2800, enter the aerobic tank for full aeration, fill the aerobic tank with 30% polyurethane filler, and stay for 17 hours.

[0057] Add 650mg / L of sodium acetate as an external carbon source to the effluent of the aerobic tank, and enter the anoxic tank to react. The anoxic tank is filled with 50% polyur...

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PUM

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Abstract

The invention relates to a method for treating high-ammonia-nitrogen wastewater by feeding a polyurethane filler. According to the method, high-ammonia-nitrogen wastewater is subjected to blowing denitrogenation pretreatment to reduce the concentration of ammonia nitrogen and to recover ammonia nitrogen; then treated ammonia-nitrogen wastewater enters an aerobic tank fed with the filler for nitration and then enters an anoxic tank fed with the filler for denitrification; so finally the wastewater reaches the standard and is then discharged. Through blowing denitrogenation pretreatment, impactof high content of ammonia nitrogen on a biochemical system can be effectively reduced, the resource of ammonia nitrogen can be recovered, and harmless and recycling treatment of the wastewater is realized; the aerobic tank and the anoxic tank are both fed with the polyurethane filler, so the concentration and stability of sludge can be improved, and the load capacity and impact resistance of thesludge can be enhanced; and after feeding of the polyurethane filler, the sludge adheres onto the polyurethane filler, so a good growth environment is formed for breeding of protists and metazoans, afood chain is extended and enriched, and the output of residual sludge is effectively reduced.

Description

technical field [0001] The invention relates to a wastewater treatment technology in the chemical industry, in particular to a method for treating wastewater with high ammonia nitrogen content by adding polyurethane fillers. Background technique [0002] Coal chemical enterprises produce a large amount of wastewater in the process of coking and gasification. These wastewaters have the characteristics of large water volume and high pollutant concentration. Among them, the ammonia nitrogen content of high ammonia nitrogen wastewater is as high as 3000-9000mg / L, which has caused huge damage to the normal operation of the enterprise and the surrounding environment. pressure. my country's coal chemical enterprises are mostly distributed in Northwest and North China. Water resources are scarce, expensive, and lack receiving water bodies. The Ministry of Environmental Protection requires coal chemical enterprises to meet the "zero discharge" standard. The problem of high ammonia n...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14
CPCC02F1/20C02F1/66C02F3/02C02F3/28C02F9/00C02F2101/16
Inventor 邱松李昕阳杨芳芳魏令勇
Owner CHINA PETROLEUM & CHEM CORP
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